Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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1-~19469 comb.
METHOD FOR TR~ATING ORG~NIC WASTE WATER BY METHANE
FERMENTATION AND TREATING APPARATUS THEREFOR
This invention relates to a method fo~ treating
organic waste water by the methane fermentation, which
method is adapted for treating organic waste water, such
as waste liquor formed in the production step of beer or
05 the like, through a biological treatment by the use of
mesophilic or thermophilic methane bacteria, and
an apparatus to be used for the method.
As the above described treating method o~
organic waste water, there are known an aerobic
treatment by the use of active sludge and an anaerobic
treatment by the use of methane bacteria. Recently,
there has been noticed a treating method, wherein
an organic substance is decomposed into methane ~as and
carbon dioxide with the use of mesophilic or
thermophilic methane bacteria by means of an anaerobic
fixed bed. However, in the case where an alcohol waste
liquor, such as wa~te liqusr formed in the production
step of be~r~ is treated by the methane fermentation,
when the BOD load is as low as about (1-3) kg/m3-day,
the treatment can be effected without trouble, but when
the BOD load is higher than about 3 kg/m3 day, the BOD
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removal ratio is gradually lowered, and a satisfactorily
high treating e~fect can not be obtained.
Japanese Patent Laid-open Application
No. 64-47,498 discloses a method for improving the
~~ efficiency of methane fermentation by adding a mineral
and a nutrient, such as amino acid or the like, to
alcohol waste liquor. However, according to the test of
this method by the inventors in the practical operation,
this method is .still unsatisfactory in the BOD load and
BOD removal.
According to the investigation by the
inventors, in the treating apparatus using an anaerobic
fixed bed of this kind, its treating ability is highly
influenced by the value of the ratio of the apparent
1~ surface area of the carrier, which carries a micro-
organism thereon, to the effective volume of the
anaerobic treating apparatusO That is, in the anaerobic
treatment, the BOD contained in waste water is
decomposed into organic acid (through acid fermentation)
by the acti.on of acid fermentation bacteria contained in
the li~uid phase, and the resulting organic acid is
decomposed into methane gas by the action of the methane
bacteria fixed to the surface of a caxrier, and
therefore it is important that the methane fermentation
in ~he second half stage proceeds in a rate higher than
~2~
the rate of the acid fermentation in the first half
stage in order to proceed smoothly the anaerobic
treatment. For this purpose, it is necessary that the
value of the ratio of the surface area of the carrier,
which is the residence of methane bacteria, to the
volume of the liquid phase, which is the residence of
acid fermentation bacteria, is not lowex than a certain
value, and it has been necessary that the value of the
ratio of (surface area of carrier)/(effective volume of
1~ liquid) is at least 20 m2/m3 as disclosed in Japanese
Patent Laid-open Application No. 63-248,497.
One of the objects of the present invention is
to solve the above described problems in the conven-
tional methods and to provide a method for treating
1~ organic waste waters by the methane fermentation, whi.ch
can treat organic waste liquors, such as waste liquor
formed in the production step of beer and the like,
in a high BOD removal ratio of not lower than 90%
while maintaining a high BOD load of not lower than
10 kg/m3-day, and a apparatus to be used for the methodO
Another object of the present invention is to
provide a method for treating organic waste waters
by the methane fermentation, which can attain the above
described object by means of an apparatus having
such a value of the ratio of (surface area of
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carrier)/(effective volurne of liquid) that is
considerably lower than the value of the ratio in the
conventional method.
The inventors have made various investigations
06 in order to solve the above described problems, and
found out that the reason why the increasing of the BOD
load results in the lowering of the BOD removal lies
in the lowering of the proliferation speed of methane
bacteria due to the shortage of nutrient, and that the
use of three elements of nickel, iron and cobalt in
amounts fairly larger than the amounts, which have
hitherto been considered to be necessary in the
conventional method, is necessary for improving
the proliferation activity of methane bacteria.
1~ The inventors have further ascertained that, when the
proliferation activity of methane bacteria, which has
been fixed to carrier, is improved by the addition of
these elements to a waste water to be treated, the vaiue
of the ratio of (surface area of carrier)/(effective
volume of liquid~ can be decreased to a value lower than
the value which has hitherto been considered to be
necessary in the conventional method.
The present invention has been accomplished
based on the above described knowledge.
The first aspect of the present invention lies
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in a method for treating an organic waste water by
a methane fermentation with the use of an anaerobic
fixed bed, an improvement comprising effecting the
treatment in the presence of nickel, iron and cobalt,
~~ which are nutrient elements necessary for the prolif-
eration of methane bacteria, while maintaining the
amounts of Ni, Fe and Co based on the BOD in the waste
water to such amounts that the value of the ratio of
Ni/~OD is at least 25x10-6r the value of the ratlo of
Fe/BOD is at least 60x10-6 and the value of the ratio of
Co/BOD is at least 1.25x10-6.
The second aspect of the present invention lies
in that the treatment of the above described first
aspect of the present invention is carried out by means
1~ of an anaerobic treating apparatus containing a carrier
packed therein r and having a value of the ratio of the
apparent surface area of the carrier to the effective
volume of the apparatus (the ratio of (surface area of
carrier)/(effective volume of liquid)) of at least
lQ m2/m3-
The third aspect of the present invention liesin an anaerobic treating apparatus to be used for
carrying out the method of the above described first
aspect o~ the present invention, whi~h apparatus
contains a carrier packed therein and has a value of the
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ratio of the apparent surface area of the carrier to the
effective volume of the apparatus (the ratio of (surface
area of carrier)/(effective volume of liquid)) of at
least l0 m2/m3.
Q~ ~he term "apparent surface area of a carrier"
herein used means the surface area of a carrier, which
i5 calculated from its geometrical shape, and does not
include the inner surface area of the carrier material
itself, which is formed by the fine small holes, cracks
and the like extending into the interior of the carrier
material. The term "effective volume of liquid" herein
used means the volume obtained by subtracting the volume
occupied by the carrier from the volume of the inner
space of the apparatus, which receives the waste water
therein together with the carrier, that isl means the
amount of waste water to be practically treated.
For a better understanding of the invention,
reference is taken to the accompanying drawings, in
which:
Fig. 1 is a diagrammatical view, partly in
section~ for explaining the treating method of the
present invention;
Fig. 2 is a graph illustrating the relation
between the value of the ratio of Ni/BOD and the BOD
26 load;
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Fig. 3 is a graph illustrating the relation
between the value o~ the ratio of Fe/BOD and the BOD
load;
Fig. 4 is a graph illustrating the relation
~~ between the value of the ratio of Co/BOD and the BOD
load;
Fig. 5 is a graph illustrating the relation
between the BOD load and the BOD removal ratio; and
Fig. 6 is a graph illustrating the relation
between the value of the ratio of (surface area of
carrier)/(effective volume of liquid) and the maximum
BOD load.
The present invention will be explained in more
detail referring to the drawings.
1~ Fig. 1 illustrates a system to be used for
carrying out a methane fermentation treatment of a waste
liquor formed in the production step of beer.
The numeral 1 represents an anaerobic treating
apparatus; the numeral 2 represents a porous ceramics
carrier containing a thermophilic methane bacteria
deposited thereon; the numeral 3 represents a storage
tank for organic waste water; the numeral 4 represents
a gas holder for receiving methane gas generated by the
methane fermentation; the numeral 5 represents a tank
for receiving a treated organic waste water; the numeral
2~2~2
6 represents a storage tank for alkali to be used for
maintaining the PH of the organic waste water in the
anaerobic treating apparatus 1 to a given PH; the
numeral 7 represents a storage tank for nutrient source;
~~ the reference PH represents a PH meter; the reference T
represents a thermometer; and the reference P represents
a pump.
The organic waste waters to be treated in the
apparatus of the present invention include waste liquors
1~ formed in the production step of beer, such as waste
liquor from slud~e trub, waste liquor from malt
dewatering process, waste beer, waste juice and their
mixtures, and the like, and further include whey waste
water from soybean process, waste water formed during
1~ the distillation in the whisky production~ and the like.
It has been found from the analysis of the components of
these waste waters that nickel, iron and cobalt are not
at all contained in these waste waters, and even in the
case where these elements are contained in the waste
waters, the amount is very small.
Therefore, in the present invention, in
addition to a commonly known nutrient source supplied
from the stcrage tank 7 for nutrient source, nickel,
iron and cobalt are occasionally added to a waste water
8~ to be treated. These elements are added to a waste
~2i3~4~
water such that the ~aste water, aft~r the addition,
contains Ni, Fe and Co in amounts, based on the BOD of
the waste water, that the value of the ratio of Ni/BOD
is at least 25x10-6, the value of the ratio of Fe/BOD is
~~ at least 60X10-6 and the value of the ratio of Co/BOD is
at least 1 a 25x10-S. Further, it is preferable to adjust
the concentrations of nitrogen and phosphorus in the
waste water to be that the value of the ratio of N/BOD
is at least 6x10-3 and the value of the ratio of P/BOD
~~ is at least 1.5x10-3.
The reason why the amounts of nickel, iron and
cobalt contained in a waste water are limited to the
above described amounts will be explained hereinafter
referring to the graphs of ~igs. 2-6, which are
1~ compilation of the data with respect to the treatments
of waste liquors, which have been forrned in the
production step of beer, by a thermophilic methane
bacteria.
As illustrated in Fig. 2, .in the re~ion wherein
the value of Ni/BOD is not lower than 25x10-6, tne BOD
load exceeds 10 kg/m3-day, but in the region wherein the
value of Ni/BOD is lower than 25x10-6, the BOD load
lowers, and in the conventional method, wherein Ni is
not at all added to the waste liquor, the sOD load is
only about 3 kg/m3~day. Fig. 3 illustrates that, in the
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region wherein the value of Fe/BOD is not lower than
60x10-6, the BOD load exceeds 10 kg/m~-day, but in the
region wherein the value of Fe/BOD is lower than
60x10-6, the BOD load lowers as well, and in the
~~ conventional method, the BOD load is only about
3 kg/m3 day. Further, as illustrated in Fig. 4, when
the value of Co/BOD is not lower than 1.25X10-6, the ~OD
load exceeds 10 kg/m3 day.
It has been ascertained that, when the above
1~ described conditions are satisfied, a high BOD removal
ratio of more than 9o% can be attained while maintaining
a high BOD load of not lower than 10 kg/m3-day.
Further, it has been able to be ascertained that,
although these data are ones with respect to
1~ thermophilic methane bacteria, data with respect to
mesophilic methane bacteria have the same tendency as
the data in the thermophilic methane bacteria.
The xeason why the addition of such relatively
large amounts of nickel, iron ancl cobalt to a waste
~~ water to be treated acts effectively is pxobably due to
the contribution of these elements to the formation of
coenzyme during the methane fermentation.
In the above described embodiments, the value
of the ratio of the apparent surface area of the porous
ceramics carrier 2 packed in an anaerobic treating
~ ~ 2 ~
apparatus 1 to the effective volume of the anaerobic
treating apparatus 1 tthe ratio of (surface area of
carrier)/~effective volume of liquid)) was set to
70 m2/m3. The inventors further measured the maxlmum
BOD load, which was able to be treated by the method of
the present invention, by changiny variously the value
of the ratio of (surface area of carrier)/(effective
volume of liquid). This measurement was carried out
under a constant condition that the value of ~i/BOD was
50x10-6, the value of Fe/BOD was 120x10-6 and the value
of Co/BOD was 2.5x10-6. For comparison, a conventional
waste water not added with nickel, iron and cobalt, and
having a value of Ni/BOD of 10x10-6, that of Fe/BOD of
~0x10-6 and that of Co/BOD of 1.0x10-4 was used, and the
1~ maximum BOD load, which was able to be treated with the
waste water, was measured in the same mannex as
described above by changing variously the value of the
ratio of (surface area of carrier)/(effective value of
liquid). The obtained results are illustrated in
~ig. 6.
It can be seen from Fig. 6 that, in the
conventional method, wherein the values of Ni/BOD,
Fe/BOD and Co/NOB are outside the range defined in the
present invention, the maximum BOD load is lower than
2~ 10 kg/m3-day unless the value of the ratio of (surface
2 3~3i83~.~
area of carrier)/(effective volume of liquid) is at
least 20 m2/m3. On the contrary, in the method of the
present invention, even when the value o~ the ratio of
(surface area of carrier)/(effsctive volume of liquid)
is 10 m2/m3~ a high maximum BOD load can be maintained.
However, even in the method of the present invention,
when the value of the ratio of (surface area of
carrier)/(effective volume of liquid) is lower than
10 m2/m3, the maximum BOD load is lower than
10 10 kg/m3 day
As described above, when the values of the
ratios of Ni/BOD, Fe/BOD and Co/BOD are within the range
defined in the present invention, the methane fermenta-
tion ability o~ methane bacteria fixed to the carrier
1~ surface is strengthened, and methane fermentation can be
satisfactorily carried out even in the case where the
amount of methane bacteria is decreased, and hence even
when the value of the ratio of (surface area of
carrier)/(effective volume of liquid) is lowered to
~~ 10 m2/m3, the methane fermentation in the second half
stage is not adversely influenced by the acid
~ermentation in the first half stage~ and a high BOD
load can be maintained.
As clearly understood from the above described
explanation, according to the present invention, the
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ratio of the amounts of nickel, iron and cobalt, which
are nutrient elements necessary for the proliferation
and the like of methane bacteria, to the BOD are
maintained to given values, whereby the proliferation
activity of methane bacteria i.s increased, and various
organic waste liquors, such as waste liqucr formed in
the production step of beer and the like, can be treated
in a high BOD removal ratio of not lower than 9o%
while maintaining a high BOD load of not lower than
10 kg/m3~day. Moreover, according to the apparatus of
the present invention, the methane fermentation ability
of methane bacteria fixed to the carrier surface has
been strengthened, and hence the value of the ratio of
(surface area of carrier)/(effective volume of liquid),
1~ which has been necessary to be not lower than 20 m2/m3
in the conventional method, can be lowered to about
10 m2/m3, and moreover various organic waste liquors can
be treated in a high BOD removal ratio while maintaining
a high BOD load.
As described above, the treating method and
apparatus of organic waste water by the methane
fermentation according to the present invention are free
from the problems in the conventional method, and the
present invention has a very high contribution to the
development of industry.
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